US2790828A - Purification of monochloroacetic acid - Google Patents
Purification of monochloroacetic acid Download PDFInfo
- Publication number
- US2790828A US2790828A US497474A US49747455A US2790828A US 2790828 A US2790828 A US 2790828A US 497474 A US497474 A US 497474A US 49747455 A US49747455 A US 49747455A US 2790828 A US2790828 A US 2790828A
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- Prior art keywords
- acid
- monochloroacetic acid
- monochloroacetic
- dichloroacetic
- purification
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/42—Separation; Purification; Stabilisation; Use of additives
- C07C51/43—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Crystallography & Structural Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
United States Patent PURIFICATION OF MONOCHLOROACETIC ACID Jerome N. Haimsohn, Ardsley, N. Y., assignor to Staufier Chemical Company, a corporation of Delaware No Drawing. Application March 28, 1955, Serial No. 497,474
5 Claims. (Cl. 260-539) This invention relates to a method of purifying monochloroacetic acid and particularly to a method of removing dichloroacetic acid from monochloroacetic acid.
In the chlorination of acetic acid to produce monochloroacetic acid, it is inevitable that some dichloro substitution takes place so that the final product is ordinarily a mixture of monochloroacetic acid and dichloroacetic acid. Technical monochloroacetic acid ordinarily contains from about 1.5% to 2.5% of dichloroacetic acid and for many purposes, it is important a purer product be obtained. Heretofore, there has been no fully satisfatcory process of purifying monochloroacetic acid. Although it has been proposed to purify monochloroacetic acid by crystallization from a solvent, the process is expensive, both from the standpoint of solvent and product losses.
It is therefore the object of the present invention to provide a simple, economical process for the purification of technical monochloroacetic acid by removing dichloroacetic acid therefrom.
It has been found that purification can be effected merely by drying the monochloroacetic acid such as by heating'the monochloroacetic acid in a vacuum drier, sweeping a stream of gas over the monochloroacetic acid, conveying the monochloroacetic acid in an air stream, or by fluidizing solid monochloroacetic acid with air or other inert gas. For this purpose, regular drying equipment can be used such as vacuum, tray, rotary, flash or other driers such as are well known to those skilled in the art for removing moisture or other volatile compounds from solids by evaporation. It is surprising that monochloroacetic acid can be purified in this way since dichloroacetic acid is higher boiling and has a lower vapor pressure than monochloroacetic acid. Thus, one would expect the monochloroacetic acid to volatilize first, but the re- :"verse has been found to be true, as is shown by the we perimental examples which follow. Although this invention is not predicated upon any theory of its operation, it is believed that the dichloroacetic acid which is present as a contaminant exists in a liquid state surrounding the monochloroacetic acid crystals. The liquid apparently has a higher effective vapor pressure than the crystalline monochloroacetic acid and can therefore be separated by evaporation, providing the monochloroacetic acid is kept in a solid state.
The process can be operated at any temperature below the melting point of monochloroacetic acid, namely 62' C. However, to secure optimum results, it is ordinarily preferred to operate at a temperature of at least 20 C.
The following non-limiting examples illustrate various embodiments of the present invention.
Example 1.0ne pound of technical monochloroacetic 2,790,828 Patented Apr. 30, 1957 Dichloro- Wt. Loss, acetic acid Percent of content, Charge Wt.
Percent Strippin Sample No. e in Example 2.Two pounds of technical monochloracetic acid containing 1.79% dichloroacetic acid was maintained in a fluidized state in a 2%" diameter, 4 foot long glass tube with dry air at 37 C. and at a rate of 4' S. C. F. M. (approximately 1.6 F. P. S., superficial velocity) for 2 Example 3.-Three hundred pounds technical monochloroacetic acid, containing 1.53% dichloroacetic acid, was passed through a pneumatic conveying drier (flash drier) at a rate of 7.5 pounds per minute with 2000 C. F. M. of air at 45 C. The inlet air had a dew-point of 0 C. Four spot samples of product from the drier had a dichloroacetic acid content of 0.501004%.
Example 4.--Fifty gram portions of commercial, technical monochloracetic acid, containing 2.06% dichloroacetic acid and 0.8% moisture, were dried in a vacuum oven at 40 C. and at a pressure of 10 mm. mercury. Results with varying degrees of drying are contained in the following table:
' Cumulative Water Percent Di- Sample No. over Wt. Loss Content, chloroon Drying, percent acetic percent Acid 0 (startin 0. 8 2.06
material Example -5.One pound technical monochloroacetic acid containing 2.00% dichloroacetic acid was fluidized in a 2.5 inch diameter, 4 ft. long glass tube at 40 C. with undried air (from a compressor), at an air rate of 1.9 cubic feet per minute (approximately 0.9 ft. per second,
Example 6.600 pounds of technical monochloroacetic ac1d, containing 1.86% dichloroacetic acid, was passed through a pneumatic conveying drier (flash drier) at a rate of 9.0 pounds per minute with 2000 C. F. M. of air at 35' C. The inlet air had a relative humidity of 10%. The product from the drier had a dichloroacetic acid content of 0.56%.
The product from the foregoing nm was passed through the flash drier a second time under identical conditions. Afterthesecondpass,theproductfromthedriercontained 0.20% acid.
I claim: a
l. The process of purifying monochloroacetic acid which contains a small percentage of dichloroacetic acid as a contaminant; comprising heating said monochloroacetic acid containing said contaminant at a temperature of not over 62' C. and dichloroacetic acid to volatilize therefrom. I
2. The process of purifying monochloroacetie acid which contains dichloroacetic acid as a contaminant comprising fluidizing said monochloroacetic acid in a gas stream at a temperature of not over 62' C.
3. The process 0! purifying monochloroacetic acid whichcontains dichloroacetic acid as a contaminant comprising heating said monochloroacetic acid in a vacuum oven at a temperature of not over 62' C.
4. The process of purifying monochloroacetic acid which contains dichloroacetic acid as a contaminant comprising passing an inert gas over the surface of said mow chloroacetic acid at a temperature of not over 62' C.
5. The process of purifying monochloroacetic acid which contains a small percentage of dichloroacetic acid as contaminant, comprising conveying sad monochloroacetic acid in a gas stream at a temperature of not over 62' C. whereby dichloroscetic acid is volatilized therefrom.
Rulers-ens (Bed In the die of thh pas-l Young: "Distillation Principles and Processes, 1922, pp. 223 and 475.
Claims (1)
1. THE PROCESS OF PURIFYING MONOCHLOROACETIC ACID WHICH CONTAINS A SMALL PERCENTAGE OF DICHLOROACETICA ACID AS A CONTAMINANT, COMPRISING HEATING SAID MONOCHLOROACETIC ACID CONTAINING SAID CONTAMINANT AT A TEMPERATUE OF NOT OVER 62*C. AND PERMITTING DICHLOROACETIC ACID TO VOLATILIZE THEREFROM.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US497474A US2790828A (en) | 1955-03-28 | 1955-03-28 | Purification of monochloroacetic acid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US497474A US2790828A (en) | 1955-03-28 | 1955-03-28 | Purification of monochloroacetic acid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2790828A true US2790828A (en) | 1957-04-30 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US497474A Expired - Lifetime US2790828A (en) | 1955-03-28 | 1955-03-28 | Purification of monochloroacetic acid |
Country Status (1)
| Country | Link |
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| US (1) | US2790828A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3002996A (en) * | 1956-07-10 | 1961-10-03 | Leuna Werke Veb | Process for the preparation of dry oximes |
| US3365493A (en) * | 1964-09-29 | 1968-01-23 | Dow Chemical Co | Manufacture of monochloroacetic acid |
| DE1268130B (en) * | 1959-12-07 | 1968-05-16 | Uddeholms Ab | Process for cleaning monochloroacetic acid |
| US3772157A (en) * | 1971-12-10 | 1973-11-13 | Dow Chemical Co | Purification of 2-chloroalkanoic acids by azeotropic distillation |
-
1955
- 1955-03-28 US US497474A patent/US2790828A/en not_active Expired - Lifetime
Non-Patent Citations (1)
| Title |
|---|
| None * |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3002996A (en) * | 1956-07-10 | 1961-10-03 | Leuna Werke Veb | Process for the preparation of dry oximes |
| DE1268130B (en) * | 1959-12-07 | 1968-05-16 | Uddeholms Ab | Process for cleaning monochloroacetic acid |
| US3365493A (en) * | 1964-09-29 | 1968-01-23 | Dow Chemical Co | Manufacture of monochloroacetic acid |
| US3772157A (en) * | 1971-12-10 | 1973-11-13 | Dow Chemical Co | Purification of 2-chloroalkanoic acids by azeotropic distillation |
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